Flue gas mercury absorption liquid with functions of oxidizing and fixing synchronously
A mercury absorption, coal-fired flue gas technology, applied in chemical instruments and methods, dispersed particle separation, separation methods, etc., can solve the problems of large consumption of oxidant, increased anti-corrosion requirements, increased absorption liquid corrosion, etc., to achieve mercury removal The effect of high removal rate
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Embodiment 1
[0040] Example 1: Fenton's reagent oxidation combined with lime slurry + sodium thiosulfate to absorb and remove mercury
[0041] The mercury removal absorption liquid used in this embodiment includes lime slurry with a mass concentration of 4%, and Fenton's reagent and sodium thiosulfate, Fe 3+ From Ferric Chloride, Fe 3+ :H 2 o 2 =0.5, the pH value of the absorption solution is 3.5, and the addition amount of Fenton’s reagent is expressed as H 2 o 2 Calculated as 0.09mol / L, the amount of sodium thiosulfate added is 0.8mol / L; under simulated conditions, the imported mercury concentration is 60μg / L, the sulfur dioxide concentration is 500ppm, and the gas volume is 2L / min, the height of the absorption liquid is 14cm, and the volume of the absorption liquid is 300ml. The removal rate of sulfur dioxide is greater than 25%, and the removal efficiency of mercury reaches 50%.
Embodiment 2
[0042] Example 2: Fenton reagent oxidation combined with limestone slurry + calcium thiosulfate to absorb and remove mercury
[0043] The mercury removal absorbing solution used in this embodiment includes limestone slurry with a mass concentration of 4%, and Fenton's reagent and sodium thiosulfate, Fe 3+ From Ferric Chloride, Fe 3+ :H 2 o 2 =0.6, the pH value of the absorption solution is 1.5, and the addition amount of Fenton's reagent is expressed as H 2 o 2 Calculated as 0.07mol / L, the amount of sodium thiosulfate added is 0.6mol / L; under simulated conditions, the imported mercury concentration is 60μg / L, absorbed by the bubble bottle, the gas volume is 2L / min, and the absorption liquid height is 14cm , the volume of the absorption liquid is 300ml, the temperature of the absorption liquid is 30°C; the removal rate of sulfur dioxide is greater than 20%, and the removal efficiency of mercury reaches 60%.
Embodiment 3
[0044] Example 3: Fenton reagent oxidation combined with calcium oxide + potassium thiosulfate to absorb and remove mercury
[0045] The mercury removal absorbing solution used in this embodiment includes a calcium oxide (calcium hydroxide after entering the solution) slurry with a mass concentration of 3%, and in the slurry, Fenton's reagent and potassium thiosulfate, Fe 3+ From ferric nitrate, Fe 3+ :H 2 o 2 =0.7, the pH value of the absorption solution is 1.5, and the addition amount of Fenton’s reagent is expressed as H 2 o 2 Calculated as 0.15mol / L, the amount of potassium thiosulfate added is 0.9mol / L; under simulated conditions, the imported mercury concentration is 60μg / L, the sulfur dioxide concentration is 500ppm, and the gas volume is 2L / min, the height of the absorption liquid is 14cm, the volume of the absorption liquid is 300ml, and the temperature of the absorption liquid is 45°C; the removal rate of sulfur dioxide is greater than 35%, and the removal effic...
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